DocumentCode :
3124176
Title :
Recovery of Dimethylbenzene/ Butylacetate from Spent Solvent Oil by Batch Distillation: Experiment and Simulation
Author :
Li Changhai ; Li Yuejin
Author_Institution :
Binzhou Univ., Binzhou, China
fYear :
2010
fDate :
18-20 June 2010
Firstpage :
1
Lastpage :
4
Abstract :
The recovery of Dimethylbenzene and Butylacetate from industry spent solvent oil by batch distillation was studied, and the batch distillation experiment was performed with pretreated material. The effect of separation temperature, time and reflux ratio on separation process was investigated. The experimental results showed that the concentrations of Dimethylbenzene and Butylacetate were above 95% in top distillate product, and the yield of Dimethylbenzene and Butylacetate was 62% and 99.45%, respectively, under appropriately conditions. A robust and rapid mathematical model had been developed, based on mass balance and relative volatility. The satisfactory results obtained allowed to use the model in real time for a better control and management of batch distillation.
Keywords :
batch processing (industrial); chemical engineering; distillation; oils; separation; solvents (industrial); batch distillation; butylacetate; dimethylbenzene; distillate product; industry spent solvent oil; mass balance; rapid mathematical model; relative volatility; robust mathematical model; separation process; time and reflux ratio; Chemical industry; Equations; Fuel processing industries; Mathematical model; Petroleum; Robustness; Separation processes; Solvents; Temperature; Volatile organic compounds;
fLanguage :
English
Publisher :
ieee
Conference_Titel :
Bioinformatics and Biomedical Engineering (iCBBE), 2010 4th International Conference on
Conference_Location :
Chengdu
ISSN :
2151-7614
Print_ISBN :
978-1-4244-4712-1
Electronic_ISBN :
2151-7614
Type :
conf
DOI :
10.1109/ICBBE.2010.5516590
Filename :
5516590
Link To Document :
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